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WO1995015351A1 - Polysulfones aromatiques - Google Patents

Polysulfones aromatiques

Info

Publication number
WO1995015351A1
WO1995015351A1 PCT/GB1994/002652 GB9402652W WO9515351A1 WO 1995015351 A1 WO1995015351 A1 WO 1995015351A1 GB 9402652 W GB9402652 W GB 9402652W WO 9515351 A1 WO9515351 A1 WO 9515351A1
Authority
WO
WIPO (PCT)
Prior art keywords
formula
polyethersulphone
membrane
comonomer
polymer
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Ceased
Application number
PCT/GB1994/002652
Other languages
English (en)
Inventor
Howard Matthew Colquhoun
David Frank Lewis
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
North West Water Group PLC
Original Assignee
North West Water Group PLC
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by North West Water Group PLC filed Critical North West Water Group PLC
Priority to AU11163/95A priority Critical patent/AU683516B2/en
Priority to EP95902228A priority patent/EP0731820B1/fr
Priority to DE69409828T priority patent/DE69409828T2/de
Priority to US08/647,976 priority patent/US5693740A/en
Priority to JP7515498A priority patent/JPH09505849A/ja
Publication of WO1995015351A1 publication Critical patent/WO1995015351A1/fr
Anticipated expiration legal-status Critical
Ceased legal-status Critical Current

Links

Classifications

    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G65/00—Macromolecular compounds obtained by reactions forming an ether link in the main chain of the macromolecule
    • C08G65/34—Macromolecular compounds obtained by reactions forming an ether link in the main chain of the macromolecule from hydroxy compounds or their metallic derivatives
    • C08G65/48—Polymers modified by chemical after-treatment
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D71/00—Semi-permeable membranes for separation processes or apparatus characterised by the material; Manufacturing processes specially adapted therefor
    • B01D71/06—Organic material
    • B01D71/66—Polymers having sulfur in the main chain, with or without nitrogen, oxygen or carbon only
    • B01D71/68—Polysulfones; Polyethersulfones
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G75/00—Macromolecular compounds obtained by reactions forming a linkage containing sulfur with or without nitrogen, oxygen, or carbon in the main chain of the macromolecule
    • C08G75/20—Polysulfones
    • C08G75/23—Polyethersulfones

Definitions

  • the present invention relates to aromatic polysulphones which are useful particularly, but not exclusively, as membranes for filtration operations.
  • Composite membranes comprising a thin film of a hydrophilic, sulphonated aromatic polyethersulphone supported on an ultrafiltration membrane are known to have good chemical stability (particularly to extremes of pH and to chlorinated feed waters) and to be usable in reverse osmosis and nanofiltration.
  • Examples of sulphonated polymers which have been used in the past to produce such membranes are shown below as Polymers A,B, and C.
  • Polymer C has particular advantages in that (i) the presence of the biphenyl linkage in place of an isopropylidene or ether linkage provides a material with significantly improved thermo-mechanical and chemical stability, (ii) the precursor (i.e. non-sulphonated) polymer is readily synthesised at high molecular weight, and (iii) sulphonation of this material to give Polymer C proceeds rapidly and cleanly at room temperature.
  • an aromatic polyethersulphone incorporating the following sub-unit I.
  • A is an electron withdrawing group
  • the designation 'o,p' represents that the bond is at the ortho or para position to the A group
  • X is selected from; -OH; -0 (M n " ) 1 / n where M is an organic or inorganic cation (other than hydrogen) and n is at least 1; -NR 1 R 2 where R. and R 2 are the same or different and are selected from hydrogen, and alkyl, aryl, aminoalkylene or ammonioalkylene groups; and -OR where R ⁇ is an alkyl or aryl group; either as the only sub-units of the polymer or in combination with comonomer units.
  • A is preferably a carbonyl linkage (-CO-) or, more preferably, a sulphonyl linkage (-S0 2 -). If X is
  • the cation may have a valency of one or more. If the valency is greater than 1 then it will be appreciated that the - O " moiety is associated with a fraction 1/n of the cation.
  • M may for example be an alkali metal, alkaline earth metal, or a higher valency metal ion, eg Al 3+ .
  • M is sodium or potassium.
  • R. and R 2 are preferably other than hydrogen. If R 2 and/or R 2 is alkyl it preferably has less than 4 carbon atoms.
  • a suitable example of an aminoalkylene group for R . and R 2 is -(CH 2 ) réelle- H 2 where m is less than 4, preferably 2.
  • a suitable ammonioalkylene group is -(CH 2 ) m -N + R 4 R 5 R 6 where R 4 , R 5 and R 6 are independently hydrogen, alkyl or aryl. If X is -0R 3 and R 3 is alkyl it preferably has less than 4 carbon atoms.
  • Polymers in accordance with the invention are hydrophilic by virtue of the presence of the -S0 2 X groups and are eminently suitable for use as membranes in filtration operations effected in an aqueous environment. Therefore according to a second aspect of the invention there is provided a porous or non-porous membrane comprising an aromatic polyethersulphone incorporating the sub-unit (I) defined above either alone or in combination with comonomer units.
  • Membranes in accordance with the second aspect of the invention may for example be asymmetric membranes, composite membranes or dense films and may be used in a variety of separation processes including reverse osmosis, electrodialysis, nanofiltration, ultrafiltration, microfiltration, gas separation, pervaporation, haemodialysis and haemofiltration.
  • a particularly preferred form of membrane in accordance with the invention is a composite membrane comprising a thin film of the polymer supported on an ultrafiltration membrane.
  • Such composite membranes are particularly suitable as reverse osmosis membranes since they have been surprisingly found not to suffer the problem of poor reverse osmosis performance associated with polymer C (see above).
  • the sub-unit (I) in the polymers of the invention is preferably of the formula (II).
  • the polymers of the invention may comprise only units (I) (or (II)) or may incorporate comonomer units, eg of the formula (III) or (IV).
  • A', A", and A'" represent the same or different electron withdrawing linkages, most preferably carbonyl (-CO-) or sulphone (-S0 2 -) linkages.
  • -CO- carbonyl
  • sulphone -S0 2 - linkages.
  • all bonds and substituents shown in formulae (III) and (IV) are (on any one aromatic ring) in para relationship to each other.
  • the comonomer unit (if present) is most preferably of the formula (VI).
  • sub- units (I) may provide 1-99%, more preferably at least 10% eg at least 25%, by mole of the total number of monomer units present in the polymer.
  • Preferred copolymers in accordance with the invention are of the formula (VII)
  • ratio is of m:n is less than 10:1, more preferably less than 4:1, eg 3:1.
  • the polymers of the invention preferably have a molecular weight of 2000 to 100,000, more preferably 5000 to 50,000.
  • the inherent viscosity of the polymers as measured at a concentration of 1% in N- methylpyrrolidone at 25°C will generally be in the range of 0.3-5.0.
  • A is an electron withdrawing linkage and Y is a leaving group either alone or in combination with at least one comonomer which is condensable therewith and which gives a substantially non- sulphonatable copolymer unit, said polycondensation or copolycondensation being effected in a solvent for the monomer; and (b) sulphonating the resultant polymer.
  • the anion of formula (VIII) is generated in situ during the polycondensation or copolycondensation from a monomer of formula (Villa)
  • a and Y are as defined above, the polycondensation being effected in the presence of a base.
  • a stoichiometric amount of the base is preferably used.
  • the base may for example be an alkali metal carbonate or an alkali metal fluoride, e.g. potassium fluoride.
  • the analogous compound in which the -S0 2 - linkage is replaced by a carbonyl linkage (i.e. -CO-) may be synthesised by the procedures described in EP-A-0 232 992 (ICI Pic).
  • Other compounds embraced by formulae (VII) and (IX) may be synthesised by procedures known in the art.
  • the anion (VIII) may be obtained by reaction of the corresponding free hvdroxy compound with a base (e.g. by reaction with the appropriate alkali metal hydroxide and removal of water) prior to the polycondensation or copolycondensation step.
  • the polycondensation or copolycondensation step will generally be effected at a temperature in the range 150-330°C, preferably 250- 300°C.
  • Comonomers which may preferably be used in step (a) are of the general formula X, XI, and XII
  • Z, Z', Z", Z*", Z"" and Z'"" are the same or different and are selected from hydroxyl groups and leaving groups (preferably halogen atoms (eg chlorine)).
  • the solvent may be a dipolar aprotic solvent as commonly used for substitution reactions, eg dimethylformamide, dimethylsulphoxide, N-methylpyrrolidone, sulpholane, dimethyl sulphone and diphenyl sulphone although other solvents which are substantially non-reactive under the reaction conditions may be employed.
  • the preferred solvent is diphenyl sulphone.
  • the reaction will generally be effected at a temperature in the range 150°-330°, preferably 250°-300°C.
  • the sulphonation step (b) is most conveniently effected using concentrated (95-100%) sulphuric acid most preferably 98% sulphuric acid. Using concentrated sulphuric acid, sulphonation occurs cleanly in high yield without degradation of the polymer. Other sulphonating agents such as oleum, sulphur trioxide, or a sulphur trioxide derivative such as S0 3 -pyridine or S0 3 -triethylphosphate may be used.
  • Sulphonation has been found to occur substantially as mono- sulphonation in one ring of the oxybiaryl residue to give a sulphonated entity as shown for sub-unit (I).
  • the actual position of substitution in that ring will be determined by the position of the other substituents therein.
  • sulphonation of a polymer obtained by condensation of a monomer of formula (IX) yields a polymer sulphonated at the position shown for sub-unit (II).
  • sulphonation is specific to the oxybiaryl residue it will be appreciated that any desired level of sulphonation of the polymer may be obtained by varying the proportion of comonomer units used in step (a).
  • a compound of the formula VIII may initially be sulphonated to give the sulphonic acid derivative which can then be condensed, optionally with comonomers as described above, to give the final polymer.
  • the aforementioned polyether sulphonyl halides are novel intermediates and are therefore provided as a further aspect of the invention.
  • membranes produced from polymers in accordance with the invention may be over-coated with a cross-linked optionally protected polyol as disclosed in WO 94/17905.
  • the polyol may for example be polyvinylalcohol and may be protected by formaldehyde.
  • the reactants were mixed with diphenyl sulphone (56 g) as solvent, blanketed with a slow purge of dry nitrogen, and heated with stirring over 5 hours to 280°C. After 30 minutes at this temperature the viscous reaction mixture was cooled to room temperature and the resulting solid was milled to a fine powder. This was extracted successively with water and then methanol at reflux, and dried to give a 11.0 g of a copolymer with inherent viscosity in N-methylpyrrolidone (NMP) of 0.66. In a second stage, 3.0 g of this material was dissolved in 50 cm 3 of 98% sulphuric acid and the resulting clear, pale yellow solution was allowed to stand for 16 hours.
  • NMP N-methylpyrrolidone
  • the membrane was dried at 80°C. On testing in reverse osmosis (2000 ppm NaCl, 40 bar) the membrane gave a water flux of 78 US gallons/ft 2 /day (GFD) and a salt rejection of 95.9%.
  • the membrane was dried at 80°C. On testing in reverse osmosis (2000 ppm NaCl, 40 bar) the membrane gave a water flux of 135 GFD and a salt rejection of 82.9%. It will thus be seen that polymer VII (i.e. one in accordance with the invention) gives superior salt rejection characteristics to one formed from polymer C in an otherwise identical membrane.
  • the inherent viscosity of this polymer in NMP was 1.23.
  • the inherent viscosity of this polymer in NMP was 1.13.
  • This Example demonstrates chlorine tolerance of a membrane based on a polymer of the invention:
  • a composite membrane prepared as in Example 1 was overcoated with formaldehyde-protected polyvinyl alcohol, as described in WO 94/17905.
  • the salt rejection of the resulting membrane on 500 ppm NaCl at 4 bar was 93.5% and the flux was 0.13 m 3 /m /day.
  • This membrane was run in reverse-osmosis at 60 psi with a feed containing 50 ppm of active chlorine at an average pH of 8.0. After a total chlorine exposure of 38,000 ppm-hrs the membrane showed a rejection of 92.7% and a flux of 0.11 m 3 /m 2 /day.

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Organic Chemistry (AREA)
  • Health & Medical Sciences (AREA)
  • Medicinal Chemistry (AREA)
  • Polymers & Plastics (AREA)
  • General Chemical & Material Sciences (AREA)
  • Polyethers (AREA)
  • Polymers With Sulfur, Phosphorus Or Metals In The Main Chain (AREA)
  • Polyoxymethylene Polymers And Polymers With Carbon-To-Carbon Bonds (AREA)
  • Separation Using Semi-Permeable Membranes (AREA)
  • Treatments Of Macromolecular Shaped Articles (AREA)
  • Addition Polymer Or Copolymer, Post-Treatments, Or Chemical Modifications (AREA)
  • Pharmaceuticals Containing Other Organic And Inorganic Compounds (AREA)

Abstract

L'inventon se rapporte à une polyéthersulfone aromatique comprenant la sous-unité (I), dans laquelle A représente un groupe soustracteur d'électrons, la désignation 'o,p' indique que la liaison est en position ortho ou para par rapport au groupe A, et X est sélectionné parmi: -OH; -O-Mn+ où M représente un cation organique ou inorganique (différent d'hydrogène) et n vaut au moins 1; -NR¿1?R2 où R1 et R2 sont identiques ou différents et sont sélectionnés parmi hydrogène, et les groupes alkyle, aryle, aminoalkylène ou ammonoalkylène; et -OR3 où R3 représente un groupe alyle ou aryle; cette sous-unité se présentant sous la forme soit de sous-unités uniques du polymère, soit est associée à des unités de comonomères. Les polymères sont utilisés dans la production de membranes destinées à des procédés de séparation.
PCT/GB1994/002652 1993-12-02 1994-12-02 Polysulfones aromatiques Ceased WO1995015351A1 (fr)

Priority Applications (5)

Application Number Priority Date Filing Date Title
AU11163/95A AU683516B2 (en) 1993-12-02 1994-12-02 Aromatic polysulphones
EP95902228A EP0731820B1 (fr) 1993-12-02 1994-12-02 Polysulfones aromatiques
DE69409828T DE69409828T2 (de) 1993-12-02 1994-12-02 Aromatische polysulfone
US08/647,976 US5693740A (en) 1993-12-02 1994-12-02 Aromatic polysulphones
JP7515498A JPH09505849A (ja) 1993-12-02 1994-12-02 芳香族ポリスルホン

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
GB9324731.0 1993-12-02
GB939324731A GB9324731D0 (en) 1993-12-02 1993-12-02 Aromatic polysulphones

Publications (1)

Publication Number Publication Date
WO1995015351A1 true WO1995015351A1 (fr) 1995-06-08

Family

ID=10746013

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/GB1994/002652 Ceased WO1995015351A1 (fr) 1993-12-02 1994-12-02 Polysulfones aromatiques

Country Status (9)

Country Link
US (1) US5693740A (fr)
EP (1) EP0731820B1 (fr)
JP (1) JPH09505849A (fr)
AT (1) ATE165380T1 (fr)
AU (1) AU683516B2 (fr)
CA (1) CA2177965A1 (fr)
DE (1) DE69409828T2 (fr)
GB (1) GB9324731D0 (fr)
WO (1) WO1995015351A1 (fr)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1999038897A1 (fr) * 1998-01-30 1999-08-05 Hydro-Quebec Polymeres sulfones reticules et leur procede de preparation

Families Citing this family (21)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP3724064B2 (ja) * 1996-06-28 2005-12-07 住友化学株式会社 燃料電池用高分子電解質及び燃料電池
US6828353B1 (en) 1998-09-11 2004-12-07 Victrex Manufacturing Limited Ion-exchange polymers
WO2000059986A1 (fr) * 1999-04-05 2000-10-12 E.I. Du Pont De Nemours And Company Production de polysulfones
US6258272B1 (en) 1999-04-09 2001-07-10 Usf Filtrations And Separations Group, Inc. Internal hydrophilic membranes from blended anionic copolymers
DE19954158A1 (de) * 1999-11-10 2001-05-17 Inst Textil & Faserforschung Mikroporöse hydrophile Membran
EP1149625B1 (fr) * 2000-04-26 2006-12-06 Pall Corporation Membranes totalement hydrophiles à partir de mélanges de copolymères anioniques
JP2004500971A (ja) * 2000-05-02 2004-01-15 ベルント・シンドラー スルホン化アリールスルホネートマトリックスおよびその製造方法
JP4689790B2 (ja) * 2000-05-02 2011-05-25 ポール・コーポレーション アニオンコポリマーブレンドの内部親水性膜
DE10296292D2 (de) * 2001-11-22 2004-12-23 Thomas Haering Modifizierte kovalent vernetzte Polymere
US20060115695A1 (en) * 2002-12-26 2006-06-01 Ube Industries, Ltd. Bisphenol compound and aromatic polyaryl ether
US20050113558A1 (en) * 2003-11-20 2005-05-26 General Electric Company Polyethersulfone composition, method of making and articles therefrom
US7902316B2 (en) * 2003-11-20 2011-03-08 Sabic Innovative Plastics Ip B.V. Polyethersulfone composition, method of making and articles therefrom
GB0400626D0 (en) * 2004-01-13 2004-02-11 Johnson Matthey Plc Polymer
US20070117962A1 (en) * 2005-11-21 2007-05-24 General Electric Company High heat polyethersulfone compositions
JP2008031452A (ja) * 2006-07-03 2008-02-14 Sumitomo Chemical Co Ltd 芳香族ブロック共重合体、その分解方法および該分解方法を用いた分析方法
US20100196782A1 (en) * 2006-08-11 2010-08-05 Toray Industries, Inc. Polymer electrolyte material, polymer electrolyte molded product using the polymer electrolyte material, and method for manufacturing the polymer electrolye molded product, membrane electrode composite, and solid polymer fuel cell
WO2008062932A1 (fr) * 2006-11-22 2008-05-29 Gwangju Institute Of Science And Technology Poly(arylène éther) sulfoné contenant une fraction réticulable dans le groupe d'extrémité, son procédé de fabrication; et utilisation du poly(arylène éther) sulfoné et de son procédé dans une membrane électrolytique polymère
US8829060B2 (en) 2011-03-01 2014-09-09 Dow Global Technologies Llc Sulfonated poly(aryl ether) membrane including blend with phenol compound
US8752714B2 (en) 2011-03-01 2014-06-17 Dow Global Technologies Llc Sulfonated poly (aryl ether) membrane including blend with phenyl amine compound
JP2013144780A (ja) * 2011-12-13 2013-07-25 Central Glass Co Ltd へキサフルオロイソプロパノール基を含むポリスルホンおよびその合成方法
KR101491782B1 (ko) * 2012-12-03 2015-02-11 롯데케미칼 주식회사 정밀여과막 또는 한외여과막 제조용 고분자 수지 조성물, 고분자 여과막의 제조 방법 및 고분자 여과막

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EP0008894A1 (fr) * 1978-09-05 1980-03-19 Imperial Chemical Industries Plc Copolymères de polyaryléthersulfone sulfonés et procédé pour leur préparation
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GB1586972A (en) * 1977-02-01 1981-03-25 Ici Ltd Production of aromatic polyethers
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EP0008894A1 (fr) * 1978-09-05 1980-03-19 Imperial Chemical Industries Plc Copolymères de polyaryléthersulfone sulfonés et procédé pour leur préparation
EP0008895A1 (fr) * 1978-09-05 1980-03-19 Imperial Chemical Industries Plc Polyaryléthercétones sulfonées et procédé pour leur préparation
GB2245577A (en) * 1990-06-26 1992-01-08 Ici Plc Polyarylsulphones

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1999038897A1 (fr) * 1998-01-30 1999-08-05 Hydro-Quebec Polymeres sulfones reticules et leur procede de preparation
US6670424B1 (en) 1998-01-30 2003-12-30 Hydro-Quebec Ross-linked sulphonated polymers and their preparation process
EP1400539A1 (fr) * 1998-01-30 2004-03-24 Hydro Quebec Polymères sulfonés réticulés et leur procédé de préparation
US7034082B2 (en) 1998-01-30 2006-04-25 Hydro-Quebec Cross-linked sulphonated polymers and their preparation process
US7674560B2 (en) 1998-01-30 2010-03-09 Hydro-Quebec Cross-linked sulphonated polymers and their preparation process

Also Published As

Publication number Publication date
US5693740A (en) 1997-12-02
JPH09505849A (ja) 1997-06-10
ATE165380T1 (de) 1998-05-15
AU683516B2 (en) 1997-11-13
GB9324731D0 (en) 1994-01-19
EP0731820A1 (fr) 1996-09-18
DE69409828D1 (en) 1998-05-28
AU1116395A (en) 1995-06-19
CA2177965A1 (fr) 1995-06-08
DE69409828T2 (de) 2000-01-27
EP0731820B1 (fr) 1998-04-22

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